US4931197A - Copolymers for α-β-unsaturated dicarboxylic acid esters wherein said esters are comprised of ethoxylated esters, methods for their production as well as their use as lubricant for the working-up of plastics - Google Patents

Copolymers for α-β-unsaturated dicarboxylic acid esters wherein said esters are comprised of ethoxylated esters, methods for their production as well as their use as lubricant for the working-up of plastics Download PDF

Info

Publication number
US4931197A
US4931197A US07/168,554 US16855488A US4931197A US 4931197 A US4931197 A US 4931197A US 16855488 A US16855488 A US 16855488A US 4931197 A US4931197 A US 4931197A
Authority
US
United States
Prior art keywords
unsaturated dicarboxylic
dicarboxylic acid
copolymers
acid ester
esters
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US07/168,554
Inventor
Heinz Beck
Karl-Heinz Frassek
Eduard M. Verhulst
Egenius A. Giezen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ITALMATCH CHEMICALS ARESE Srl (ICA SRL)
Original Assignee
Akzo NV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to DE3136931A priority Critical patent/DE3136931C2/de
Priority to DE3136931 priority
Application filed by Akzo NV filed Critical Akzo NV
Application granted granted Critical
Publication of US4931197A publication Critical patent/US4931197A/en
Anticipated expiration legal-status Critical
Assigned to ITALMATCH CHEMICALS ARESE S.R.L. (I.C.A. S.R.L.) reassignment ITALMATCH CHEMICALS ARESE S.R.L. (I.C.A. S.R.L.) ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AKZO NOBEL NV
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F222/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
    • C08F222/10Esters
    • C08F222/12Esters of phenols or saturated alcohols
    • C08F222/20Esters containing oxygen in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/14Monomers containing five or more carbon atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L101/00Compositions of unspecified macromolecular compounds

Abstract

The copolymers of the invention are made from α,β-unsaturated dicarboxylic acid esters and α-olefins. The α-olefins employed have 8 to 24 C-atoms and the α,β-unsaturated dicarboxylic acid esters are made solely from ethoxylated alcohol with a degree of ethoxylation of 1 to 45. Also disclosed is a process for the production of these copolymers, in which either α-olefin having 8-24 C-atoms is copolymerized with α-β-unsaturated dicarboxylic anhydride or α-β-unsaturated dicarboxylic acid at temperatures of 80°-210° C. in the presence of a peroxide catalyst in an inert gas atmosphere, along with esterification with ethoxylated alcohol having a degree of ethoxylation of 1-45 in the mole ratio of 1:1 to 1:2 α-β-unsaturated dicarboxylic acid or anhydride : ethoxylated alcohol, or by copolymerizing α-olefins having 8-24 C-atoms and α-β-unsaturated dicarboxylic acid ester having ethoxylated alcohol with a degree of ethoxylation from 1 to 20 as alcohol component at temperatures of 140°-210° C. in the presence of a peroxide catalyst in an inert gas atmosphere. The copolymers are preferably used as lubricant for the shaping treatment of thermoplastic plastics.

Description

This application is a continuation of application Ser. No. 418,401, filed Sept. 15, 1982, now abandoned.
BACKGROUND OF THE INVENTION
The invention concerns copolymers from α-β-unsaturated dicarboxylic acid esters with α-olefins, their production and their use as lubricants for the shaping treatment of plastics.
Olefin-maleic acid-copolymer derivatives are known from German Offenlegungsschrift DE-OS No. 27 27 239, which are constructed from olefins with an average of 2-24 carbon atoms and maleic acid and are esterified with univalent alcohols having a chain length from 2-20 carbon atoms in the mole ratio 1:0.5 up to 1:2 maleic acid to alcohol. The described olefin-maleic acid-copolymer derivatives are produced through copolymerization of maleic acid anhydride with α-olefins and connected esterification into semi- or diester. The there described olefin-maleic acid-copolymer derivatives are particularly suitable as lubricants for the shaping working-up of plastics.
Beyond that, high-molecular copolymers from α-olefins and α-β-unsaturated dicarboxylic acid esters have been known for example as hair sprays (AU-PS No. 254,327) and as coating agents for medicines (AU-PS No. 263,011). These were produced by copolymerization of α-olefins and α-β-unsaturated dicarboxylic acids or acid anhydrides and subsequent esterification of the copolymers.
German Offenlegungsschrift DE-OS No. 17 70 860 discloses a copolymerisate of a C22 -C28 -1-olefin and dibehenylmaleate, which was obtained by polymerization at 150° C. It was suggested to add the product to hydrocarbons, in order to lower the solidification point or totally improve the flowability.
AU-PS No. 479,746 describes copolymerisate from α-β-unsaturated dicarboxylic acid esters having one or two straight-chain ester groups with 18-44 C-atoms with C18 -C46 -α-olefins as flowability improver for wax-like hydrocarbon oil, the copolymerisate effecting a lowering of the pour point of the hydrocarbon oil.
Numerous substances have already been suggested as lubricants for the shaping working-up of plastics. With regard to their characteristics, they display more or less great differences, or possess in many respects advantages in contrast to others. One significant characteristic is the compatibility of lubricants with determined stabilizers, which are likewise mixed in for the deformation of plastics in order to avoid degradation phenomena resulting from the stress and strain occurring upon deformation. As stabilizers, for example metal salts or metalloorganic compounds are used. One known type of stabilizer, which is used for the stabilization of PVC (polyvinyl chloride), is composed from tin compounds. Many, even of these tin, stabilizers are not well compatible with lubricants. Those stabilizers for which this applies in particular measure include, for example, dibutyl tin-di-monomethylmaleate. In order to be able to produce mixtures with lubricants, both stable and of good dosability, also with these stabilizers, which are very approved in practice, efforts have for a long time been made--without great success--to test lubricants which would make such mixtures possible.
SUMMARY OF THE INVENTION
It has now been determined that copolymerisates of α-β-unsaturated dicarboxylic acid esters and α-olefins, which are thereby characterized in that they are constructed from α-olefins having 8-24 C-atoms and from α-β-unsaturated dicarboxylic acid esters, the alcohol components of which are ethoxylated alcohols with a degree of ethoxylation from 1-45, preferably 1-20, are outstandingly suitable lubricants for such mixtures.
In preferred manner, the copolymers are so constructed that α-β-unsaturated dicarboxylic acid esters are α-β-unsaturated dicarboxylic acid diesters. The esters of maleic acid, fumaric acid, citraconic acid, mesaconic acid, or itaconic acid come into consideration as examples of α-β-unsaturated dicarboxylic acid esters. Preferably, however, the esters of maleic acid and fumaric acid are used.
Copolymers in which the α-olefin is unbranched are preferred. The copolymers which are constructed from 10-16 C-atoms display particularly good compatibility with the stabilizers. In preferred manner, the mole ratio α-olefin to α-β-unsaturated dicarboxylic acid esters amounts to 0.5-4.
The polymers according to the present invention are accessible in two manners, one being namely through copolymerization of α-β-unsaturated dicarboxylic acids or their anhydrides followed by esterification with ethoxylated alcohols having a degree of ethoxylation of 1-45. By degree of ethoxylation should be understood the number of ethenoxide units of a (poly)-ethylene oxide chain, which is etherified on one end with an alcohol, while the hydroxyl group at the other end of the (poly)ethylene oxide chain is esterified with the acid group.
Using this manner of production one obtains with the polymers a ratio of α-olefins to α-β-unsaturated dicarboxylic acid esters in the copolymers of about 1:1.
Such a method is thereby characterized according to the present invention in that α-olefins having 8-24 C-atoms and α-β-unsaturated dicarboxylic acids are copolymerized at temperatures of 80°-210° C. in the presence of a peroxide catalyst in an inert gas atmosphere, and in connection therewith are esterified with ethoxylated alcohol having a degree of ethoxylation of 1-45 in the mole ratio from 1:1 up to 1:2 α-β-unsaturated dicarboxylic acid (or anhydride):ethoxylated alcohol.
The other manner of producing the polymers according to the present invention proceeds from already esterified α-β-unsaturated dicarboxylic acid esters, which are copolymerized with α-olefins.
This process is thereby characterized in that α-olefins having 8-24 C-atoms and α-β-unsaturated dicarboxylic acid ester, the alcohol component of which is ethoxylated alcohol having a degree of ethoxylation of 1-20, are copolymerized at temperatures of 140°-210° C., preferably 160°-200° C., in the presence of a peroxide catalyst and in an inert gas atmosphere.
In this manner copolymers are also accessible in which the ratio of α-olefin to α-β-unsaturated dicarboxylic acid ester in the copolymers lies between 0.5 and 4. Such products are extensively liquid at room temperature.
Although the amounts of peroxide catalyst otherwise lies within the scope of customary additives, it is preferred within the scope of the present invention to limit the amount of peroxide to the range from 0.005 to 0.05 mole/mole monomer. Preferably, the peroxide catalyst is added portionwise in time intervals. According to one particular embodiment of the present invention, the addition of the peroxide catalyst follows in such manner that, initially, it is started through the addition of 1/3 of the amount of peroxide catalyst, and the remaining amount of peroxide catalyst is added in 8-12 portions.
In order to arrive at mole ratios of α-olefin to α-β-unsaturated dicarboxylic acid ester from 0.5 to 4 in the polymers, the monomers are used in the mole ratio 0.5-7.
On the basis of their viscosity behavior and their ability to emulsify, the copolymers according to the present invention are useful as additive for the lowering of the pour point with both mineral oils and lubricants.
As most important area of use for the copolymers according to the present invention, mention should be made mainly of lubricants for the shaping treatment of thermoplastic plastics. This comes to light still more strongly in the following examples, whereby in particular is highlighted the good compatibility with such tin stabilizers which contain ligands at the tin having bonding considered to be more ionic than covalent. The copolymers according to the present invention are emulsifiable and provide stable emulsions. They are therefore useful in mixture with waxes and with the copolymers according to German Offenlegungsschrift DE-OS No. 27 27 239 in polishing wax preparations such as, for example, shoecare agents, floor care agents, and lubricants for the working-up of metal, among others. They can also serve in aqueous emulsions as cooling agent for the cutting, machining and similar deformations of metal parts.
The novel features which are considered characteristic for the invention are set forth in particular in the appended claims. The invention itself, however, both as to its construction and its method of operation, together with additional objects and advantages thereof, will be best understood from the following description of specific embodiments.
DESCRIPTION OF THE PREFERRED EMBODIMENTS EXAMLE 1
This Example describes the production of copolymers in which the relative amounts of α-olefin to α-β-unsaturated dicarboxylic acid ester amounts to 1:1, and the half esters are formed.
One mole of an C14/16 -α-olefin mixture (average molecular weight 205) is heated in a reaction vessel, after rinsing with nitrogen, to the reaction temperature of 150° C. Then 10 portions, each of 0.1 mole maleic acid anhydride with 0.005 mole di-t-butylperoxide, are added at 30 minute intervals. About 30 minutes after the last addition, one mole of the ethoxylated alcohol is added, after which a temperature of 150° C. is maintained a further 2 hours. In the mentioned manner, the copolymers tabulated in the following summary are produced.
______________________________________Designation      α-Olefin                Ethoxylated Alcohol______________________________________1A         C14/16    ethylglycol1B         C14/16    methylglycol1C         C14/16    methyldiglycol1D         C14/16    methoxypolyethyleneglycol,                ethoxylation degree = 71E         C15/16    methoxypolyethyleneglycol,                ethoxylation degree = 12______________________________________
EXAMPLE 2
In this Example the production of copolymers is described, for which the ratio of α-olefin to α-β-unsaturated dicarboxylic acid ester can deviate from the ratio 1:1 and for which α-β-unsaturated dicarboxylic acid diesters are copolymerized with the α-olefins.
5 mole maleic acid anhydride (or an equivalent amount of fumaric acid), 14 mole of an ethoxylated alcohol, 25 g p-toluenesdulfonic acid and 500 ml toluene are mixed together and heated to boiling temperature. The reaction water and, with connection of a vacuum, the toluene and the excess alcohol, are distilled off. The mixture is then heated to 160° C. and the α-olefin is added. The reaction vessel is rinsed with nitrogen and in 11 portions at intervals of 30 minutes each, 0.03 mole di-t-butylperoxide is added. 30 minutes after the last peroxide addition the excess α-olefin is distilled off in a vacuum. A coloration--particularly with low ratios α-olefin to α-β-unsaturated dicarboxylic acid ester--can be avoided through addition of sodium hypophosphite after the esterification.
According to the previously described process, the copolymers tabulated in the following summary were produced:
______________________________________Desig-         Ethoxylated Monomer Polymerisationnation α-Olefin          Alcohol     Ratio   Temperature______________________________________2A    C10      ethylglycol 3:1     1702B    C10      ethylglycol 2.59:1  1702C    C10      ethylglycol 1:1     1702D    C10      methylglycol                      1:1     1702E    C10      methyldiglycol                      3:1     1702F    C10      methyldiglycol                      1:1     1702G    C12      ethylglycol 1:1     2002H    C12      methylglycol                      1:1     2002I    C12      methyldiglycol                      1:1     2002K    C12      methyldiglycol                      3:1     2002L    C14/16   methylglycol                      0.82:1  2002M    C14/16   methylglycol                      1:1     2002N    C14/16   methylglycol                      0.68:1  2002O    C14/16   ethylglycol 1:1     2002P    C14/16   ethylglycol 0.68:1  2002Q    C14/16   ethylglycol 0.5:1   1602R    C14/16   methyldiglycol                      1:1     200______________________________________
EXAMPLE 3
The copolymers produced according to Examples 1 and 2 were tested for their compatibility with sulfur-free tin stabilizers. Dibutyltin dimonomethylmaleate served therewith as sample substance.
After mixing the copolymers with the stabilizer in different weight ratios at 90° C., the samples are cooled to room temperature and then left 1 week at room temperature.
It is then observed whether a phase separation follows or whether a precipitation has occurred.
It was determined that with all of the copolymers according to Examples 1 and 2 at weight ratio 1:1 copolymer to tin stabilizer, neither a phase separation nor a precipitation had occurred. At weight ratio 1:3 copolymer to tin stabilizer, the same result is obtained for the copolymers 1E; 2C; 2D; 2E; 2H; 2I; 2L; 2N; and 2R; whereas with the other copolymers at with weight ratio a turbidity is visible.
EXAMPLE 4
The behavior of plastic masses upon deformation from the melt can be determined by measurements in the "Brabender Plasticorder". In this Example there are described measurements which were performed on plastic masses formed from 100 parts by weight PVC suspension, 2 parts by weight dibutyltin dimonomethylmaleate, and portions of 0.5 parts by weight of one of the copolymers according to Examples 1 and 2. For purposes of comparison, a commerically available lubricant is tested in the same manner. The results are summarized in Table 1, wherein the designation I is used for the commercially available lubricant. It involves therewith an ethylene glycol ester of montanic acid.
Lubricants intrinsically lower the melt viscosity. This is manifested with measurements in the "Brabender Plasticorder" in that a small force is necessary. In addition, lubricants increase the gelation time and decrease the adhesion of the plastic to the wall.
In the "Brabender Plasticorder" the following conditions are maintained:
______________________________________Temperature       160° C.Velocity          15 revolutions/minuteSample Weight     31 g______________________________________
The following Tables 1 and 2 show the results with regard to gelation time, moment of rotation upon gelation, gelation temperature, torque 10 minutes after the gelation, and temperature 10 minutes after the gelation.
In addition, the transparency of test disks of 3 mm thickness is measured at a wavelength of 690 nm.
                                  TABLE 1__________________________________________________________________________ Gelation      Torque           Temperature                   Torque Temperature Time upon upon Gelation                   10 min. after                          10 min. after                                 TransparencyCopolymer (min.)      Gelation           (°C.)                   Gelation                          Gelation                                 (%)__________________________________________________________________________1A    5.7  2500 156     2700   160    761B    5.4  2650 155     2700   160    781C    6.7  2550 155     2800   160    781D    7.2  2400 156     2700   160    811E    8.8  2400 156     2700   160    82__________________________________________________________________________
                                  TABLE 2__________________________________________________________________________ Gelation      Torque  Temperature                      Torque Temperature Time upon    upon Gelation                      10 min. after                             10 min. after                                    TransparencyCopolymer (min.)      Gelation (m · g)              (°C.)                      Gelation                             Gelation                                    (%)__________________________________________________________________________I     6.9  2600    155     2750   160    742A    11   2500    155     2750   160    742C    5.5  2600    155     2775   159    842D    5.1  2500    155     2750   160    812E    7.1  2500    154     2750   160    802F    4.4  2550    153     2750   159    842G    6.9  2600    154     2700   160    812H    5.2  2600    154     2775   159    832I    5.3  2600    154     2800   160    842K    6.4  2600    155     2700   160    812L    4.9  2600    154     2750   160    842M    5.1  2500    154     2750   160    882N    5.1  2600    155     2750   160    882O    7.4  2500    155     2700   160    792P    6.3  2500    155     2700   160    822R    6.0  2600    155     2700   160    87__________________________________________________________________________
EXAMPLE 5
The suitability of the copolymers as lubricant is also shown with the mill test. For this purpose, mixtures are produced from 100 parts by weight of a suspension of PVC, 1.5 parts by weight dibutyltin dimethylmonomaleate, 0.5 or 1 part by weight of the copolymer or a commercial lubricant, as well as 1 part by weight of a fatty alcohol or glycerine monofatty acid ester and 1 part by weight polymethacrylate as flowing agent. For the mill test the following conditions are adjusted:
______________________________________Temperature of the     180° C.front rollTemperature of the     176° C.rear rollClearance width        0.9 mmRatio of friction      1:1Rotational speed       15 rpm______________________________________
Every 5 minutes the samples are withdrawn, and the test is terminated when the sample has stuck to the roller or when a brown coloration is observed. The results are set forth in the following Table 3.
              TABLE 3______________________________________                            Melting   Parts                    temperature   by       Time until sticking                            at endCopolymer   Weight   (minutes)       of the test______________________________________I       0.5      15              187I       1.0      30 (brown, no sticking)                            1862A      0.5      25              1882A      1.0      35 (brown, no sticking)                            1862C      0.5      35 (brown, no sticking)                            1882C      1.0      35 (brown, no sticking)                            1882D      0.5      20              1872E      0.5      18              1862F      0.5      15              1862F      1.0      25              1872G      0.5      20              1862L      1.0      10              1862O      0.5      15              1862O      1.0      30 (brown, no sticking)                            1872P      0.5      20              1872P      1.0      30 (brown, no sticking)                            1872R      0.5      10              1862R      1.0      10              1861A      0.5      25              1861B      0.5      25              1861C      0.5      20              1861D      0.5      30 (brown, no sticking)                            1861E      0.5      25              186______________________________________
It will be understood that each of the elements described above, or two or more together, may also find a useful application in other types of polymers differing from the types described above.
While the invention has been illustrated and described as embodied in copolymers from α, β-unsaturated dicarboxylic acid esters, processes for their production as well as their use as lubricant for the working-up of plastics, it is not intended to be limited to the details shown, since various modifications and structural changes may be made without departing in any way from the spirit of the present invention.
Without further analysis, the foregoing will so fully reveal the gist of the present invention that others can, by applying current knowledge, readily adapt it for various applications without omitting features, that, from the standpoint of prior art, fairly constitute essential characteristics of the generic or specific aspects of this invention.
What is claimed as new and desired to be protected by Letters Patent is set forth in the appended claims.

Claims (20)

We claim:
1. Copolymers of:
a. α-olefin hydrocarbons having 8 to 24 carbon atoms, and
b. α, β-unsaturated dicarboxylic acid esters having an alcohol component, said alcohol component thereof consisting of ethoxylated alcohols having a degree of ethoxylation from 1 to 45 and wherein ethoxylated alcohol esters are the sole ester group present, wherein the mole ratio of α-olefin hydrocarbon to α, β-unsaturated dicarboxylic acid ester in said copolymers is from 0.5 to 4.
2. Copolymers according to claim 1, wherein the α, β-unsaturated dicarboxylic acid esters are β-α-unsaturated dicarboxylic acid diesters.
3. Copolymers according to claim 1, wherein the α-β-unsaturated dicarboxylic acid ester is maleic acid ester and fumaric acid ester.
4. Copolymers according to claim 1, wherein the α-β-unsaturated dicarboxylic acid ester is maleic acid ester or fumaric acid ester.
5. Copolymers according to claim 1, wherein the α-olefins are unbranched.
6. Copolymers according to claim 1, wherein the α-olefins are constructed with 10-16 carbon atoms.
7. Copolymers according to claim 1, wherein the degree of ethoxylation is from 1 to 20.
8. Method for the production of copolymers from α-β-unsaturated dicarboxylic acid esters and α-olefin hydrocarbons according to claim 1, comprising copolymerizing α-olefin hydrocarbons having 8-24 C-atoms and α-β-unsaturated dicarboxylic acid anhydride or α-β-unsaturated dicarboxylic acid at temperatures of 80°-210° C. in the presence of a peroxide catalyst in an inert gas atmosphere, and esterifying with ethoxylated alcohol having a degree of ethoxylation of 1-45 in a mole ratio from 1:1 up to 1:2 α-β-unsaturated dicarboxylic acid or anhydride: ethoxylated alcohol.
9. Method for the production of copolymers from α-β-unsaturated dicarboxylic acid ester and α-olefin hydrocarbons according to claim 1, comprising copolymerizing α-olefin hydrocarbons having 8-24 C-atoms and α-β-unsaturated dicarboxylic acid esters having ethoxylated alcohol with a degree of ethoxylation of 1-20 as alcohol component at temperatures of 140°-210° C, in the presence of a peroxide catalyst in an inert gas atmosphere.
10. Method according to claim 9, using as α-β-unsaturated dicarboxylic acid ester α-β-unsaturated dicarboxylic acid diester as monomer.
11. Method according to claim 9, using maleic acid ester and fumaric acid ester as α-β-unsaturated dicarboxylic acid ester.
12. Method according to claim 9, using maleic acid ester or fumaric acid ester as α-β-unsaturated dicarboxylic acid ester.
13. Method according to claim 8 or claim 9, using unbranched α-olefin hydrocarbon.
14. Method according to claim 8 or claim 9, wherein 0.005 mole/mole monomer up to 0.05 mole/mole monomer of peroxide catalyst is added.
15. Method according to claim 8 or claim 9, wherein the peroxide catlayst is added portionwise at time intervals.
16. Method according to claim 15, wherein the copolymerization is started through the addition of one third of the amount of peroxide catlyst and the remainder or peroxide catalyst being added in 8-12 portions.
17. Method according to claim 8 or claim 9, using α-olefin hydrocarbon having 10-16 C-atoms.
18. Method according to claim 9, wherein the reaction temperature is 160°-200° C.
19. Method according to claim 9, using α-olefin and α-β-unsaturated dicarboxylic acid ester in a mole ratio of 0.5-7.
20. In a method of shaping treatment of thermoplastic plastics of a type employing a lubricant, the improvement wherein copolymers from α-β-unsaturated dicarboxylic acid esters and α-olefin hydrocarbons according to claim 1 are employed as said lubricant.
US07/168,554 1981-09-17 1988-03-04 Copolymers for α-β-unsaturated dicarboxylic acid esters wherein said esters are comprised of ethoxylated esters, methods for their production as well as their use as lubricant for the working-up of plastics Expired - Lifetime US4931197A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
DE3136931A DE3136931C2 (en) 1981-09-17 1981-09-17
DE3136931 1981-09-17

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US06418401 Continuation 1982-09-15

Publications (1)

Publication Number Publication Date
US4931197A true US4931197A (en) 1990-06-05

Family

ID=6141909

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/168,554 Expired - Lifetime US4931197A (en) 1981-09-17 1988-03-04 Copolymers for α-β-unsaturated dicarboxylic acid esters wherein said esters are comprised of ethoxylated esters, methods for their production as well as their use as lubricant for the working-up of plastics

Country Status (9)

Country Link
US (1) US4931197A (en)
EP (1) EP0075216B1 (en)
JP (1) JPH0339094B2 (en)
AT (1) AT14442T (en)
AU (1) AU551880B2 (en)
CA (1) CA1239740A (en)
DE (1) DE3136931C2 (en)
ES (1) ES515756A0 (en)
ZA (1) ZA8206087B (en)

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5093019A (en) * 1988-12-08 1992-03-03 Mitsubishi Kasei Corporation Liquid separating agent consisting essentially of a copolymer of an α-
US5274102A (en) * 1993-02-19 1993-12-28 Akzo Nv Epoxy functional copolymer of higher α-olefin and unsaturated dicarboxylic acid ester and derivatives thereof
US5368757A (en) * 1991-03-22 1994-11-29 Henkel Corporation Lubrication for cold forming of metals
WO1995014762A1 (en) * 1993-11-22 1995-06-01 Colgate-Palmolive Company Liquid cleaning compositions
US5435928A (en) * 1981-09-17 1995-07-25 Akzo Nobel N.V. Copolymers from α-β-unsaturated dicarboxylic acid esters, and their use
US5446105A (en) * 1994-02-18 1995-08-29 Akzo Nobel N.V. Functionalized copolymer of higher α-olefin and unsaturated dicarboxylic acid ester and derivatives thereof
WO1996007722A1 (en) * 1994-09-02 1996-03-14 Henkel Corporation Composition and process for lubricating metal before cold forming
US5547595A (en) * 1995-02-07 1996-08-20 Henkel Corporation Aqueous lubricant and process for cold forming metal, particularly pointing thick-walled metal tubes
US5573702A (en) * 1993-11-22 1996-11-12 Colgate-Palmolive Co. Liquid cleaning compositions with grease release agent
US5575939A (en) * 1992-10-29 1996-11-19 Chemische Fabrik Stockhausen Gmbh Process for softening/stuffing leather and fur skins
WO2001044575A1 (en) * 1999-12-16 2001-06-21 Akzo Nobel N.V. Sizing composition
US6444024B1 (en) 1999-12-16 2002-09-03 Akzo Nobel Nv Sizing composition
US6458174B1 (en) * 1999-01-19 2002-10-01 Clariant Gmbh Copolymers, and their use as additives for improving the cold-flow properties of middle distillates
US20030017271A1 (en) * 2001-07-02 2003-01-23 Akzo Nobel N.V. Pigment composition
US20040266955A1 (en) * 2003-06-27 2004-12-30 Nelson Kenneth D. Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
EP2395068A1 (en) 2011-06-14 2011-12-14 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2013093103A1 (en) 2011-12-22 2013-06-27 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2017083084A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
WO2017083085A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
WO2017083086A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
FR3074809A1 (en) * 2017-12-11 2019-06-14 Total Marketing Services GREASE COMPOSITION HAVING ENHANCED ADHESIVITY

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2156823B (en) * 1984-03-22 1987-11-25 Mitsubishi Chem Ind Wax and ink composition for thermal ink transfer abstract of the disclosure
EP0181037B1 (en) * 1984-11-05 1989-08-16 Akzo N.V. Metal carboxylate derivative for use in synthetic materials, emulsions and suspensions
EP0217585A3 (en) * 1985-09-24 1989-08-30 Du Pont Canada Inc. Manufacture of film from linear low density polyethylene
JP2741631B2 (en) * 1990-11-06 1998-04-22 株式会社エヌエムビー Cement dispersant that prevents flowability deterioration
JP2741630B2 (en) * 1990-11-06 1998-04-22 株式会社エヌエムビー An agent for preventing a decrease in fluidity of a cement composition
EP0492712A1 (en) * 1990-12-24 1992-07-01 Akzo Nobel N.V. Peroxide compositions with ethoxylated water-soluble polymers
DE4139601C2 (en) * 1991-11-30 1994-09-08 Hoechst Ag Copolymers and their use as lubricants and release agents for the processing of thermoplastics
JP2007077216A (en) * 2005-09-13 2007-03-29 Daido Chem Ind Co Ltd Cold rolling oil for steel plate

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442558A (en) * 1944-04-05 1948-06-01 Prophylactic Brush Co Plasticized copolymers of compounds containing a single ch2=c< group and diesters ofethylene alpha beta dicarboxylic acids
US2542550A (en) * 1947-12-31 1951-02-20 Standard Oil Dev Co Esters of polyether acids and process
US2543964A (en) * 1947-07-09 1951-03-06 Socony Vacuum Oil Co Inc Mineral oil compositions containing copolymers of olefins and esters of alpha, beta-unsaturated polybasic acids
GB663702A (en) * 1949-09-10 1951-12-27 Standard Oil Dev Co Improvements in or relating to copolymers and to lubricant compositions containing them
US3010906A (en) * 1955-03-09 1961-11-28 Exxon Standard Sa Lubricating oil additives
US3197409A (en) * 1963-03-28 1965-07-27 California Research Corp Alkylene glycol ester reaction product

Family Cites Families (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL72274C (en) * 1949-07-26 1952-06-16
FR1101261A (en) * 1954-03-18 1955-10-04 Onera (Off Nat Aerospatiale) Improvements to liquids with lubricating properties
US2978395A (en) * 1954-10-01 1961-04-04 Exxon Research Engineering Co Gamma ray polymerization of styrene with unsaturated esters
GB848638A (en) * 1958-09-03 1960-09-21 Exxon Research Engineering Co Process of polymerizing compounds possessing a polymerizable double bond
DE1645212B2 (en) * 1963-01-18 1975-03-06 Deutsche Texaco Ag, 2000 Hamburg
US3356637A (en) * 1963-05-27 1967-12-05 Monsanto Co Vinyl chloride interpolymers and process
US3341309A (en) * 1966-03-11 1967-09-12 Exxon Research Engineering Co Terpolymer pour point depressant and method of manufacture
US3532656A (en) * 1967-01-19 1970-10-06 Gulf Research Development Co Ammonium hydroxide polymer solutions for floor polish compositions
GB1112749A (en) * 1967-04-25 1968-05-08 Shell Int Research Lubricant compositions
FR1572843A (en) * 1967-07-24 1969-06-27
US3634052A (en) * 1968-04-03 1972-01-11 Mobil Oil Corp Liquid petroleum hydrocarbon compositions containing esters of an alkyl itaconate-maleic anhydride copolymer as fluidity improvers
US3642726A (en) * 1969-08-11 1972-02-15 Gulf Research Development Co Thermoplastic crosslinked polyester material and method of molding
US3642635A (en) * 1970-03-05 1972-02-15 Exxon Research Engineering Co Synthetic petrolatum compositions
US3705853A (en) * 1970-09-23 1972-12-12 Mobil Oil Corp Grease compositions
GB1402917A (en) * 1971-06-30 1975-08-13 Gaf Corp Partial alkyl and alkoxyalkyl esters and mixed esters of interpolymers of maleic anhydride with unsaturated compounds
US3854893A (en) * 1972-06-14 1974-12-17 Exxon Research Engineering Co Long side chain polymeric flow improvers for waxy hydrocarbon oils
DE2251010C3 (en) * 1972-10-18 1980-02-14 Basf Ag, 6700 Ludwigshafen
CA1070664A (en) * 1974-09-16 1980-01-29 Marvin F. Smith (Jr.) Viscosity index additives for lubricating oils
GB1526788A (en) * 1974-10-17 1978-09-27 Exxon Research Engineering Co Lubricating compositions
US4184993A (en) * 1975-09-18 1980-01-22 Rohm And Haas Company Plasticizer, plasticized resin composition and process for preparation thereof
DE2639804A1 (en) * 1975-09-18 1977-03-31 Rohm & Haas POLYMERS
CA1099047A (en) * 1977-03-11 1981-04-07 Thomas E. Kiovsky Epr dispersant vi improver
DE2727329C2 (en) * 1977-06-16 1984-03-01 Akzo Gmbh, 5600 Wuppertal, De
JPS548132A (en) * 1977-06-21 1979-01-22 Asahi Kagaku Kogyo Kk Preventing composition for corrosion
JPS549131A (en) * 1977-06-22 1979-01-23 Asahi Kagaku Kogyo Kk Anti-corrosion composition
DE3003797C2 (en) * 1980-02-02 1983-05-11 Akzo Gmbh, 5600 Wuppertal, De

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442558A (en) * 1944-04-05 1948-06-01 Prophylactic Brush Co Plasticized copolymers of compounds containing a single ch2=c< group and diesters ofethylene alpha beta dicarboxylic acids
US2543964A (en) * 1947-07-09 1951-03-06 Socony Vacuum Oil Co Inc Mineral oil compositions containing copolymers of olefins and esters of alpha, beta-unsaturated polybasic acids
US2542550A (en) * 1947-12-31 1951-02-20 Standard Oil Dev Co Esters of polyether acids and process
GB663702A (en) * 1949-09-10 1951-12-27 Standard Oil Dev Co Improvements in or relating to copolymers and to lubricant compositions containing them
US3010906A (en) * 1955-03-09 1961-11-28 Exxon Standard Sa Lubricating oil additives
US3197409A (en) * 1963-03-28 1965-07-27 California Research Corp Alkylene glycol ester reaction product

Cited By (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5435928A (en) * 1981-09-17 1995-07-25 Akzo Nobel N.V. Copolymers from α-β-unsaturated dicarboxylic acid esters, and their use
US5093019A (en) * 1988-12-08 1992-03-03 Mitsubishi Kasei Corporation Liquid separating agent consisting essentially of a copolymer of an α-
US5368757A (en) * 1991-03-22 1994-11-29 Henkel Corporation Lubrication for cold forming of metals
US5575939A (en) * 1992-10-29 1996-11-19 Chemische Fabrik Stockhausen Gmbh Process for softening/stuffing leather and fur skins
US5274102A (en) * 1993-02-19 1993-12-28 Akzo Nv Epoxy functional copolymer of higher α-olefin and unsaturated dicarboxylic acid ester and derivatives thereof
US5334682A (en) * 1993-02-19 1994-08-02 Akzo Nv Epoxy functional copolymer of higher A-olefin and unsaturated dicarboxylic acid ester and derivatives thereof
US5573702A (en) * 1993-11-22 1996-11-12 Colgate-Palmolive Co. Liquid cleaning compositions with grease release agent
US5486307A (en) * 1993-11-22 1996-01-23 Colgate-Palmolive Co. Liquid cleaning compositions with grease release agent
WO1995014762A1 (en) * 1993-11-22 1995-06-01 Colgate-Palmolive Company Liquid cleaning compositions
US5446105A (en) * 1994-02-18 1995-08-29 Akzo Nobel N.V. Functionalized copolymer of higher α-olefin and unsaturated dicarboxylic acid ester and derivatives thereof
US5531912A (en) * 1994-09-02 1996-07-02 Henkel Corporation Composition and process for lubricating metal before cold forming
WO1996007722A1 (en) * 1994-09-02 1996-03-14 Henkel Corporation Composition and process for lubricating metal before cold forming
US5547595A (en) * 1995-02-07 1996-08-20 Henkel Corporation Aqueous lubricant and process for cold forming metal, particularly pointing thick-walled metal tubes
US6458174B1 (en) * 1999-01-19 2002-10-01 Clariant Gmbh Copolymers, and their use as additives for improving the cold-flow properties of middle distillates
WO2001044575A1 (en) * 1999-12-16 2001-06-21 Akzo Nobel N.V. Sizing composition
US6444024B1 (en) 1999-12-16 2002-09-03 Akzo Nobel Nv Sizing composition
US20030017271A1 (en) * 2001-07-02 2003-01-23 Akzo Nobel N.V. Pigment composition
US7863390B2 (en) 2003-06-27 2011-01-04 Chevron Oronise Company LLC Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
US20040266955A1 (en) * 2003-06-27 2004-12-30 Nelson Kenneth D. Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
US7256242B2 (en) 2003-06-27 2007-08-14 Chevron Oronite Company, Llc Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
US20080009427A1 (en) * 2003-06-27 2008-01-10 Chevron Oronite Company, Llc Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
US20090181869A1 (en) * 2003-06-27 2009-07-16 Chevron Oronite Company Llc Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
US7674863B2 (en) 2003-06-27 2010-03-09 Chevron Oronite Company Llc Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
SG130032A1 (en) * 2003-06-27 2007-03-20 Chevron Oronite Co Esterified copolymers of polyalkenes/unsaturated acidic reagents useful as lubricant and fuel additives
EP2395068A1 (en) 2011-06-14 2011-12-14 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2013093103A1 (en) 2011-12-22 2013-06-27 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2017083084A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
WO2017083085A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
WO2017083086A1 (en) 2015-11-13 2017-05-18 Exxonmobil Research And Engineering Company High viscosity base stock compositions
US10294438B2 (en) 2015-11-13 2019-05-21 Exxonmobil Research And Engineering Company High viscosity base stock compositions
US10301557B2 (en) 2015-11-13 2019-05-28 Exxonmobil Research And Engineering Company High viscosity base stock compositions
US10301550B2 (en) 2015-11-13 2019-05-28 Exxonmobil Research And Engineering Company High viscosity base stock compositions
US10450513B2 (en) 2015-11-13 2019-10-22 Exxonmobil Research And Engineering Company High viscosity base stock compositions
US10557100B2 (en) 2015-11-13 2020-02-11 Exxonmobil Research And Engineering Company High viscosity base stock compositions
FR3074809A1 (en) * 2017-12-11 2019-06-14 Total Marketing Services GREASE COMPOSITION HAVING ENHANCED ADHESIVITY
WO2019115398A1 (en) 2017-12-11 2019-06-20 Total Marketing Services Grease composition having improved adhesiveness

Also Published As

Publication number Publication date
JPS5861111A (en) 1983-04-12
EP0075216A2 (en) 1983-03-30
EP0075216A3 (en) 1983-08-10
ZA8206087B (en) 1983-07-27
AU551880B2 (en) 1986-05-15
AT14442T (en) 1985-08-15
CA1239740A1 (en)
DE3136931C2 (en) 1990-08-09
ES515756D0 (en)
EP0075216B1 (en) 1985-07-24
ES8307846A1 (en) 1983-07-01
JPH0339094B2 (en) 1991-06-12
DE3136931A1 (en) 1983-04-07
CA1239740A (en) 1988-07-26
ES515756A0 (en) 1983-07-01
AU8851582A (en) 1983-03-24

Similar Documents

Publication Publication Date Title
US3448047A (en) Lube oil dispersants
EP0153176B1 (en) Middle distillate compositions with improved cold flow properties
US5688887A (en) Reactive, low molecular weight, viscous poly(1-olefins) and copoly(1-olefins) and their method of manufacture
US6043401A (en) Reactive, low molecular weight, viscous poly(1-olefins) and copoly(1-olefins) and their method of manufacture
EP0030099B1 (en) Additive combinations and fuels containing them
CN101421309B (en) Dispersion stabilizer
EP0095253B1 (en) Polyethylene blend and film
EP1554320B2 (en) Liquid and gel-like low molecular weight ethylene polymers
US6730739B2 (en) Cling film with enhanced polyisobutylene tackifier
EP0604408B1 (en) Alpha-olefin polymers
US2985625A (en) Composition comprising derivatives of cross-linked carboxylic acid anhydride polymers and method of preparing same
US3790359A (en) Middle distillate fuel having increased low temperature flowability
US4880903A (en) Polyketone from carbon monoxide and mixture of olefins
US6020404A (en) Bitumen/polymer compositions with improved stability and their application in carrying out surfacing operations
US5134209A (en) Process of producing ethylene-propylene rubbery copolymer
US2213423A (en) Hydrocarbon copolymer composition
US4036910A (en) Block copolymers as viscosity index improvers for lubrication oils
EP0152180B1 (en) Polyvinyl alcohol alloys
EP0146620B1 (en) Interpolymers of ethylene and unsaturated carboxylic acids
US2839512A (en) Vinylpyridine long chain acrylic ester copolymers and their preparation
US3250715A (en) Terpolymer product and lubricating composition containing it
KR100434165B1 (en) Bifunctional additive and additive composition and flammable material which impart heat resistance to fuel
US4132663A (en) Mineral oil compositions having improved pour point containing alpha-olefin copolymers
US3322711A (en) Polymer oxidation process and emulsion therefrom
SU543356A3 (en) Depressorna additive to oil and oil products

Legal Events

Date Code Title Description
STCF Information on status: patent grant

Free format text: PATENTED CASE

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

FPAY Fee payment

Year of fee payment: 12

REMI Maintenance fee reminder mailed
AS Assignment

Owner name: ITALMATCH CHEMICALS ARESE S.R.L. (I.C.A. S.R.L.),

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:AKZO NOBEL NV;REEL/FRAME:021050/0566

Effective date: 20061220